Continuous polyamidation process - i

Abstract

A continuous process for the manufacture of a polyamide, the process comprising the steps of: (i) flowing a stream A comprising a molten dicarboxylic acid, or a molten dicarboxylic acid-rich mixture comprising a dicarboxylic acid and a diamine, through a first stage and at least one more reaction stage of a vertical multistage reactor, wherein the first stage is at the top of the reactor; (ii) counter-currently flowing a stream B comprising a diamine as either a vapour or a diamine-rich liquid through at least one of the stages below the first reaction stage of said vertical multistage reactor; (iii) accumulating a liquid phase material P comprising polyamide at and / or below the final stage of said reactor; wherein said reactor is equipped with internal features suitable for effecting contact between counter-currently flowing streams A and B; and wherein said process further comprises the step of agitating said liquid phase material P by injecting a gaseous stream C comprising steam, or at least one inert gas, or a mixture of steam and at least one inert gas into the reactor at or below the final stage of the reactor. The invention further provides a vertical multistage reactor configured to implement said process.

Description

FIELD OF THE INVENTION[0001]The present invention relates to methods for the production of polyamides, and apparatus in which the polymerisation process can be conducted. More particularly, the present invention relates to continuous processes for the production of high molecular weight polyamides by the reaction of a dicarboxylic acid with a diamine via counter-current flow in a vertical multistage reactor.BACKGROUND OF THE INVENTION[0002]Polyamides, such as nylon-6,6, require starting monomers of two kinds, a monomer having a pair of carboxylic acid functional reactive groups (diacid) and a monomer having a pair of amino functional reactive groups (diamine), and such polyamides are typically referred to as dimonomeric polyamides. The polyamide may further incorporate more than one diacid and more than one diamine and may incorporate a small amount, usually no more than 10%, of a third kind of starting material having a carboxylic acid functional group and an amino functional group...

AI Technical Summary

Benefits of technology

The invention simplifies the design and operation of reactors, allows for larger reactors to be built, and increases output while reducing energy requirements and costs. It also improves the heat transfer and reduces sensitivity to materials in the reactor. The technical effects of the invention allow for larger and more efficient production of polyamide.

Problems solved by technology

However, the post-evaporation pressure reduction step requires excessive heat to prevent the product from solidifying, and this heating is known to cause discoloration and chemical degradation of the product.

However, the high temperatures required to retain the component(s) in melt form can result in degradation, and a number of methods (see, for instance, U.S. Pat. No. 4,131,712, U.S. Pat. No. 4,433,146 and U.S. Pat. No. 4,438,257) have sought to reduce such degradation and overcome associated difficulties.

Gel build-up occurs because, without direct means for controlling the chemical equilibria in the melt, the temperature rises due to the heat emitted by the polyamidation reaction which in turn causes evaporation of water produced by the polyamidation reaction thus causing a rise in viscosity and gel build-up.

However, there are several disadvantages associated with the use of mechanical agitation, including reactor complexity and complexity in process scale-up.

Agitators used in vertical multistage polyamidation reactors are complicated and expensive to design and manufacture as they require adequate mechanical strength to sufficiently agitate molten polyamide, but minimal surface area and roughness in order to limit the extent to which their surface provides nuclei for gelation.

However, as the size of the agitator is increased to cope with the increased size of the reactor, it becomes increasingly difficult to transmit the torque generated by the agitator across the diameter of the column.

Moreover, as the size of the mechanical agitator increases, its mechanical strength must also increase, which leads to difficulties in the design, fabrication and reliability of the component, as well as increased capital expenditure.

The effective limit on the size of the mechanical agitator in turn limits the size of the polyamidation reactor, and hence the production output.

In addition, processes and apparatus using conventional mechanical agitation are sensitive to perturbations of material in the reactor, and can suffer from poor reliability.

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